Phase I — Electrical & Electromechanical (1966–1969)
Thermomagnetic systems, relays, and control methods that foreshadowed later materials research.
- US 3,356,889 — Color Television Degaussing Means (1967)
- US 3,445,740 — Step‑by‑Step Thermo‑Magnetic Motor (1969)
- US 3,480,891 — Relay with Contacts of Mercury Metal Composition (1969)
Phase II — Mercury‑Aluminum Chemistry (1971)
Foundational chemistry around aluminum‑copper‑mercury complexes.
- US 3,574,607 — Aluminum‑Copper‑Mercury Complex (1971)
Phase III — Activated Aluminum & Industrial Chemistry (1972–1978)
Activated aluminum processes, peroxides, halohydrates, organoiodides, and pollutant capture systems.
- US 3,856,841 — Aluminum Organoiodides (1974)
- US 3,957,598 — Metal Hydrates & Carboxylic Acids (1976)
- US 3,959,093 — Aluminum Hydrates & Carboxylic Acids (1976)
- US 3,969,387 — Metallic‑Organo‑Peroxide (1976)
- US 3,993,595 — Activated Aluminum (1976)
- US 4,012,487 — SO2 Removal Process (1977)
- US 4,017,527 — Metallic‑Organo‑Peroxide (1977)
- US 4,017,591 — Activated Aluminum Processes (1977)
- US 4,032,623 — Hydroperoxy Aluminum Compound (1977)
- US 4,038,373 — Aluminum Halohydrate (1977)
- US 4,053,570 — Aluminum Halohydrate (1977)
- US RE29,389 — Aluminum Organoiodides (Reissue, 1977)
- US 4,071,668 — Aluminum‑Containing Alkenylbenzene Resin (1978)
- US 4,072,699 — Aluminum Organoiodides (1978)
- US 4,093,702 — Gaseous Pollutant Removal (1978)
- US 4,093,707 — Peroxide‑Containing Aluminum Complex (1978)
- US 4,108,969 — SO2 Removal Process (1978)
Phase IV — Multi‑Metal Polymeric Complexes (1975–1978)
Complexes with NH/PH/SH functional groups, oxygen‑containing bleaches, and inorganic polymers.
- US 4,029,747 — Inorganic Monomeric & Polymeric Complexes (1977)
- US 4,116,859 — Oxygen‑Containing Bleach (1978)
- US 4,117,088 — Hydrophosphide Multi‑Metal Complex (1978)
- US 4,117,099 — Hydrosulfide Multi‑Metal Complex (1978)
Later Industrial Applications (1979–1982)
Electrolytic complexes, detergent systems, and oil recovery methods.
- US 4,180,444 — Electrolytic Methods with Graphitic Carbon Cathodes (1979)
- US 4,182,685 — Metal‑Containing Soap (1980)
- US 4,317,487 — Oil & Hydrocarbon Recovery (1982)